JP2009165449A - Method and apparatus for producing biomineral - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for producing a biomineral by which the highly safe biomineral can be produced by sufficiently removing harmful materials by the heating and filtering of a raw material. <P>SOLUTION: The apparatus for producing the biomineral is configured of a first pulverizer 100 for pulverizing organisms, a heater 200 for heating the pulverized powder, a filter device 300 for filtering a mixed liquid of the heated and ashed powder with a liquid, an evaporator 400 for compulsorily evaporating the water content in the filtrate extracted by the filter device 300, and a second pulverizer 500 for pulverizing the residue from which the water content is removed into a powder shape. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

  The present invention relates to a method for producing a biological mineral by burning a living organism, and more particularly to a method for producing a biological mineral capable of sufficiently removing impurities contained in the living organism and a manufacturing apparatus therefor.

  In general, many kinds of minerals are known as minerals that are necessary and useful for the biological activities of organisms. When these minerals are ingested, they are usually ingested from food in animals, particularly in the human body. However, since it is practically difficult to consume all the minerals necessary for the human body from the general diet, it is artificially manufactured by chemical synthesis for the treatment and prevention of human health disorders due to mineral deficiencies. Often supplemented with minerals. However, this method has disadvantages such as poor absorption in vivo, most of it is excreted together with feces and urine, or a rejection reaction as a foreign substance.

  On the other hand, minerals are most naturally absorbed into the human body through animals that have eaten plants and animals from the earth, water, and seawater through plants or food chains, but these animals and plants do not necessarily contain the required amount of minerals. However, many animals and plants may contain a large amount of toxic and harmful substances other than minerals for inorganic or organic human bodies. Ingestion is also difficult.

  For this reason, attempts have been made to extract and collect minerals by burning and ashing plants and animals that contain effective minerals, but the collected minerals are limited to a single mineral, At present, it has not been fully put into practical use because its type and amount are unstable.

In order to solve such a problem, as disclosed in Patent Document 1, a “biological mineral production method” derived from a living organism that has a high absorption rate into the human body and is safe has been proposed.
In the “biological mineral production method” of Patent Document 1, an organism containing one or more kinds of minerals is heated at a temperature equal to or lower than a heating upper limit temperature at which the mineral to be extracted and collected out of the minerals is gasified and disappears. In the method for producing a biological mineral, the organic component of the biological body is removed by extraction, and the mineral to be collected is distilled and collected. Mineral is extracted and collected by heating at a heating upper limit temperature at which the mineral can be extracted, and separately by heating at a heating upper limit temperature at which other types of minerals can be extracted from the organism, By mixing both minerals, minerals with a heating upper limit temperature at least above the heating point are reliably extracted and collected, and minerals below that It provides clarity that does not remain and the stability of minerals contained in it, and more highly purified minerals can be extracted and mixed from raw organisms that contain a large amount of specific minerals. I can do it.
Japanese Patent No. 3084687

  However, according to the method for producing a biomineral proposed in Patent Document 1, although the raw material is heated at the upper heating limit temperature, harmful substances are removed by gasification, and the raw material is incinerated and purified and extracted. There is a problem that it takes time to uniformly ash the raw material simply by heating the raw material at the heating upper limit temperature. In addition, it is difficult to remove harmful substances only by heating. And there is a problem that the biological mineral produced in this way is not sufficient from the viewpoint of safety.

  The present invention has been made in view of such problems, and a method for producing a biomineral capable of sufficiently removing harmful substances in a relatively short time and producing a highly safe and highly pure biomineral and its production An object is to provide an apparatus.

  In order to achieve the above-mentioned object, the present invention provides a method for producing a biological mineral in which a biological material containing a plurality of types of minerals is heated and extracted and collected. A heating step for heating until the powder is incinerated, a filtration step for filtering a mixed liquid by mixing a liquid with the ashed powder, and evaporating the filtered filtrate And a second pulverizing step for pulverizing the residue remaining after the evaporation. The method for producing a biomineral is characterized by comprising:

  In the above configuration, when the powder is heated, it is desirable to heat the powder in two stages at different temperatures, and it is desirable to extract the filtrate by filtering the mixed solution a plurality of times.

  In order to achieve the above object, the present invention provides a biological mineral manufacturing apparatus for heating and collecting a biological body containing a plurality of types of minerals, and pulverizing the biological body into a powder. A first pulverizing unit; a heating unit that heats the powder pulverized by the pulverizing apparatus until ashing; and a liquid mixture mixed with the powder ashed by the heating unit is filtered. Filtering means, evaporating means for evaporating the filtrate filtered by the filtering means, and second pulverizing means for pulverizing the residue remaining after evaporation by the evaporating means. An apparatus for producing biological minerals is provided.

  In the above configuration, the filtering means preferably includes a plurality of filtration devices connected in series, and the heating means preferably heats the powder in two stages at different temperatures.

  According to the present invention, the organism is pulverized into a powder, heated until the powder is incinerated, a liquid is mixed with the incinerated powder, and the mixed liquid is filtered and filtered. The residue remaining after the evaporation of the filtrate was evaporated, and the impurities contained in the organism could be sufficiently removed by heating and filtration. Minerals can be provided.

Next, a biomineral production method and a biomineral production apparatus according to the present embodiment will be described with reference to the drawings.
FIG. 1 is a schematic configuration diagram of a biomineral production apparatus to which the biomineral production method according to the present embodiment is applied.
This biomineral production apparatus 10 heats the first pulverizer 100 that pulverizes raw seaweed (or seaweed) and vegetation into a powder, and the powder pulverized by the first pulverizer 100. Then, the heating device 200 that removes impurities, and the filtration device 300 that filters the mixed liquid obtained by mixing the powder heated by the heating device 200 to remove impurities and high-temperature water supplied from a liquid tank 305 described later. And an evaporation device 400 for evaporating the filtrate obtained from the filtration device 300, and a second pulverization device 500 for further pulverizing the residue obtained from the evaporation device 400 into a fine powder. Yes.

  The first pulverizer 100 pulverizes raw seaweed (or seaweed), vegetation, and the like into a powder form. A hopper 102 that inputs and accumulates raw materials and a pulverizer 101 installed below the hopper 102. It consists of. The raw material charged into the hopper 102 is pulverized by the pulverizer 101 until it becomes powder, and the pulverized powder is fed into the heating device 200.

  As described above, the heating device 200 is a device that removes impurities contained in the powder by heating the powder fed from the first pulverizer 100. Powder, nitrogen gas, and a deoxidizing agent are mixed in the heating device 200 to make the heating device 200 in an oxygen-free state, and the powder is heated. In the heating device 200, primary heating for heating the powder at a temperature of 300 to 500 ° C. and secondary heating for further heating the powder at a temperature higher than the heating temperature of the primary heating (600 to 800 ° C.) are performed. It is. Impurities generated in the heating device 200, for example, impurities such as agricultural chemicals, tar, iodine, etc. are removed by primary heating, and a powder completely ashed by secondary heating is obtained. The powder completely incinerated by the secondary heating is sent to the filtration device 300.

  The filtration device 300 is a filtration device that mixes high-temperature water with the powder ashed by the heating device 200 and filters the mixed solution, and filters the mixed solution over four stages. Device 304, liquid tank 305 for supplying high-temperature water to primary filtration device 301 to fourth filtration device 304, and storage tank 306 for storing filtrate taken from primary filtration device 301 to fourth filtration device 304 It consists of and.

  A pump 307 and a solenoid valve 308 are connected in series to the primary filtration device 301 to the fourth filtration device 304, respectively. The primary filtration device 301 is connected to the heating device 200, and the primary filtration device is connected to the primary filtration device 301. A secondary filtration device is connected, a tertiary filtration device is connected to the secondary filtration device, a fourth filtration device 304 is connected to the tertiary filtration device, and the fourth filtration device 304 becomes a terminal filtration device. ing. And the high temperature water from the liquid tank 305 is supplied to the liquid mixture sent to the back | latter stage filtration apparatus from a front | former stage filtration apparatus, respectively. In addition, the soot (residue) contained in the mixed solution sent from the preceding filtration device to the subsequent filtration device flows into the lower filtration device from the joke filtration device while precipitating at the bottom of each filtration device 301 to 304, and finally Thus, the water is discharged from the fourth filtration device 304 to the outside through the pump 307 and the solenoid valve 308.

Further, the primary filtration device 301 to the fourth filtration device 304 include a filter 309 for filtering the mixed liquid discharged from each filtration device, and a pump 310 for sending the filtrate filtered by the filter 309 to the storage tank 306. And a filtration mechanism comprising a solenoid valve 311 for controlling opening and closing of the pump 310 is connected to each other. In addition, by electronically controlling the pump 307 and the solenoid valve 308, it is possible to adjust the amount of movement of the mixed liquid in each of the filtration devices 301 to 304, and by electronically controlling the pump 310 and the solenoid valve 311, The amount of the filtrate extracted from each of the filtration devices 301 to 304 can be adjusted.

As described above, since the filtration mechanism is connected to each filtration device, the mixed solution that could not be sufficiently filtered by the upper filtration device can be filtered by the lower filtration device. A large amount can be taken out to the storage tank 306 in a short time.
The number of primary filtration devices 301 to quaternary filtration device 304 is four in this embodiment, but the number is not limited to one as long as it is one or more. Also, the connection form of each filtration device may be any connection form as long as it is in a serial form, and is not limited to the above.

  The evaporation device 400 is a device that heats and evaporates the filtrate taken out from the filtration device 300 and stored in the storage tank 306, and passes the filtrate stored in the storage tank 306 via the pump 401 and the solenoid valve 402. A predetermined amount is taken out and heated to evaporate. Since the filtrate stored in the storage tank 306 contains powder as well as liquid, only the liquid is evaporated by the evaporator 400, and as a result, dried powder remains.

The second pulverizing apparatus 500 is an apparatus that further pulverizes the powder obtained by the evaporation apparatus 400 into a fine powder, and includes a pulverizer 501 for this purpose. This pulverizer 501 is a pulverizer capable of obtaining a powder finer than the powder obtained by the pulverizer 100, similar to the pulverizer 101 provided in the first pulverizer 100. In this way, biominerals can be obtained by fine pulverization with the second pulverizer 500.

Next, with reference to FIG. 2, the manufacturing method of the biological mineral using this biological mineral manufacturing apparatus is demonstrated.
FIG. 2 is a diagram showing a flowchart of a method for producing a biomineral. A method for producing biominerals will be described with reference to the drawings.

<Crushing process>
First, a raw material (seaweed or vegetation) weighed in advance is introduced into the hopper 102 of the first crusher 100 as needed (step S100). The charged raw material is pulverized by a pulverizer 101 provided in the first pulverizer 100 to be powdered and fed into the heating device 200.

<Heating process>
Next, in the heating device 200, the obtained powder is heated at two stages of heating temperatures (step S101). First, nitrogen gas (N 2 gas) and a deoxidizing agent (carbon powder (CO 2) or silicon (SiO 2)) are mixed into the heating device 200 together with the powder to make the inside of the heating device 200 oxygen-free, and the powder is made 300 to 300- Heat at a temperature of 500 ° C. (primary heating).
Primary heating generates a lot of smoke and tar that is removed. In the primary heating, since the powder is solidified by the salt contained in the seaweed that is the raw material, the heating is not uniform. For this reason, the powder solidified after the primary heating is roughly crushed.

  And powder is further heated at the temperature (600-800 degreeC) higher than the heating temperature of primary heating (secondary heating). The powder can be uniformly heated by the secondary heating, and becomes a completely ashed powder, which is sent to the filtration device 300.

<Filtration process>
Next, the ashed powder delivered from the heating device 200 and the pre-weighed high-temperature water from the liquid tank 305 are sent to the primary filtration device 301 to form a mixed liquid of the powder and high-temperature water, and filtered. Is started (step S103).

  In the primary filtration device 301, the filtrate is taken out through the filter 309, and the mixed solution that could not be filtered is sent to the secondary filtration device 302, and further, pre-weighed high-temperature water from the liquid tank 305 is added thereto. The filtrate is taken out through the filter 309. This process is repeated in each filtration device, and the remaining residue liquid is taken out by the quaternary filtration device 304. In the filtration process in these primary filtration devices 301 to 304, the oxygen scavenger mixed in the heating device 200 is removed.

  The filtrate taken out from the primary filtration device 301 to the fourth filtration device 304 is stored in the storage tank 306 and is retained in the storage tank 306 for a predetermined time, thereby precipitating the powder contained in the filtrate.

<Evaporation process-2nd crushing process>
In the evaporator 400, a predetermined amount of filtrate and precipitated powder stored in the storage tank 306 is taken out via the pump 401 and the solenoid valve 402, and heated to evaporate water (step S104). The substance remaining after the evaporation of water is high-purity minerals, and these are further pulverized into powder by the second pulverizer 500 (step S105).

  Thus, according to the present embodiment, the raw material is heated at different temperatures such as primary heating and secondary heating in the heating device, thereby removing the agricultural chemicals, tar, iodine and harmful substances, and heating the raw material uniformly. It is possible to remove the unnecessary substances such as oxygen scavengers and remove the unnecessary substances such as oxygen scavengers by using a multi-stage filtration device. High minerals can be extracted.

It is the schematic which showed the structure of the biological mineral manufacturing apparatus. It is the flowchart which showed the manufacturing method of the biological mineral.

Explanation of symbols

DESCRIPTION OF SYMBOLS 10 Biomineral production apparatus 100 1st grinding | pulverization apparatus 101 Crusher 102 Hopper 200 Heating apparatus 300 Filtration apparatus 301 Primary filtration apparatus 302 Secondary filtration apparatus 303 Tertiary filtration apparatus 304 Fourth filtration apparatus 305 Liquid tank 306 Storage tank 307 Pump 308 Solenoid Valve 309 Filter 310 Pump 311 Solenoid valve 400 Evaporator 401 Pump 402 Solenoid valve 500 Second crusher 501 Crusher

Claims (6)

In a method for producing a biomineral that extracts and collects an organism containing multiple types of minerals by heating,
A first crushing step for crushing the organism into powder,
A heating step of heating until the powder is incinerated;
A filtration step of mixing a liquid with the ashed powder and filtering the mixed liquid;
An evaporation step of evaporating the filtered filtrate;
A second grinding step for grinding the residue remaining after the evaporation;
A method for producing a biological mineral, comprising:   The method for producing a biomineral according to claim 1, wherein when the powder is heated, the powder is heated in two stages at different temperatures.   The method for producing a biomineral according to claim 1, wherein the filtrate is extracted by filtering the mixed solution a plurality of times. In an apparatus for producing a biological mineral for heating and collecting an organism containing multiple types of minerals,
First crushing means for crushing the organism into powder,
Heating means for heating the powder pulverized by the pulverizer until ashing;
A filtering means for filtering the mixed liquid obtained by mixing a liquid with the powder ashed by the heating means;
Evaporating means for evaporating the filtrate filtered by the filtering means;
Second crushing means for crushing the residue remaining after evaporation by the evaporating means;
An apparatus for producing a biological mineral, comprising:   The biomineral production apparatus according to claim 4, wherein the filtration means includes a plurality of filtration devices connected in series.   The bio-mineral production apparatus according to claim 4, wherein the heating means heats the powder in two stages at different temperatures.

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